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WO2013049424A1 - Conversion catalytique de la cellulose en carburants et en produits chimiques avec des acides boroniques - Google Patents

Conversion catalytique de la cellulose en carburants et en produits chimiques avec des acides boroniques Download PDF

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WO2013049424A1
WO2013049424A1 PCT/US2012/057674 US2012057674W WO2013049424A1 WO 2013049424 A1 WO2013049424 A1 WO 2013049424A1 US 2012057674 W US2012057674 W US 2012057674W WO 2013049424 A1 WO2013049424 A1 WO 2013049424A1
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mgci
hmf
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WO2013049424A4 (fr
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Ronald Raines
Benjamin CAES
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Wisconsin Alumni Research Foundation
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D307/38—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
    • C07D307/40—Radicals substituted by oxygen atoms
    • C07D307/46—Doubly bound oxygen atoms, or two oxygen atoms singly bound to the same carbon atom
    • C07D307/48—Furfural
    • C07D307/50—Preparation from natural products
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/02—Boron or aluminium; Oxides or hydroxides thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/90—Regeneration or reactivation
    • B01J23/92—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/20—Carbon compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/28—Regeneration or reactivation
    • B01J27/32—Regeneration or reactivation of catalysts comprising compounds of halogens
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/12—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides
    • B01J31/14—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron
    • B01J31/146—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides of aluminium or boron of boron
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D307/38—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
    • C07D307/40—Radicals substituted by oxygen atoms
    • C07D307/46—Doubly bound oxygen atoms, or two oxygen atoms singly bound to the same carbon atom
    • C07D307/48—Furfural
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/60—Reduction reactions, e.g. hydrogenation
    • B01J2231/64—Reductions in general of organic substrates, e.g. hydride reductions or hydrogenations
    • B01J2231/641—Hydrogenation of organic substrates, i.e. H2 or H-transfer hydrogenations, e.g. Fischer-Tropsch processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/06—Halogens; Compounds thereof
    • B01J27/08—Halides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/0201—Impregnation
    • B01J37/0209—Impregnation involving a reaction between the support and a fluid
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/584—Recycling of catalysts

Definitions

  • HMF 5-(hydroxymethyl)furfural
  • HMF can be transformed into a variety of useful products including acids, aldehydes, alcohols, and amines, such as common polyester building blocks 2,5- furandicarboxylic acid, 2,5-bis(hydroxymethyl)furan, and 2,5-bis(hydroxymethyl)
  • Furfural is perhaps the most common industrial chemical derived from lignocellulosic biomass with an annual production of more than 200,000 t (Kamm et al. 2006). The conversion of pentoses into furfural has been reported (Sproull et al, 1985; Moreau et al, 1988; Mansilla et al. 1998; Dias et al. 2007). Most industrial processes achieve yields in the range of 50 molar %, which may be limited by homopolymerization and condensation with unreacted xylose. In typical processes reported, Bronsted acidic catalysts were used in aqueous solution at
  • the conversion of cellulose to HMF proceeds through three steps: hydrolysis of cellulose to glucose, isomerization of glucose to fructose, and dehydration of fructose to HMF (see Scheme 1, FIG. 1, below).
  • a number of processes have been reported to transform glucose and fructose into HMF, though few processes can access HMF in high yields directly from cellulose (Moreau et al, 2000; Seri et al, 2001; Watanabe et al, 2005a; Watanabe et al, 2005b; Yan et al, 2009; Tyrlik et al, 1999; Hu et al, 2009; Stahlberg et al. 2010; Zhao et al. 2007; Pidko et al, 2010).
  • Both xylan and xylose can be dehydrated into furfural (Zeitsch, 2000; Mamman et al. 2008).
  • Scheme 2 illustrates the formation of furfural from xylan and xylose.
  • the C-2 hydroxyl group is displaced to form a xylose-2,5-anhydride and subsequent dehydration steps produce furfural (Antal et al, 1991; Nimlos et al, 2006).
  • Boric acid is an environmentally benign catalyst that is utilized for the dehydration of alcohols (Brandenberg & Galat, 1950; O'Connor & Nace, 1955).
  • boric acid and phenylboronic acid have both been reported to be inhibitory towards the hydrolysis of cellulose and the dehydration of sugar monomers in a non-aqueous medium; and inhibition was indicated to be due to the stability of cyclic boronate esters to decomposition and dehydration (Kawamoto et al. 2008a; Kawamoto et al. 2008b). More specifically, Kawamoto et al. 2008a reports that boric acid inhibited acid-catalyzed depolymerization of cellulose, and inhibited the formation of dehydration products, including HMF, in sulfolane at high
  • the present invention provides methods for producing furans, including HMF and/or furfural, from carbohydrates including glucose, fructose and other sugars, oligosaccharides, such as cellobiose, polysaccharides, such as cellulose, hemicellulose and xylan, and lignocellulosic biomass employing certain substituted phenylboronic acids, particularly certain 2-substituted (ort/zo-substituted) phenylboronic acids, to enhance conversion to the furans.
  • the substituted phenylboronic acids are those carrying a 2- nitro, 2-alkyl, 2-alkoxy, 2-haloalkyl, a 2-aminocarbonyl, a 2-, 3-, 4- or 5-haloalkyl group, a 2-, 3- or 4-carboxy or a 2-, 3-, or 4-alkoxycarbonyl group.
  • the substituted phenylboronic acids are 2-substituted phenylboronic acids.
  • the substituted phenylboronic acids as described above can in addition carry one to four and more preferably one or two, additional substitutents as defined below.
  • the phenylboronic acid is optionally in the form of a hydrate (e.g., a monohydrate) or a salt.
  • Preferred 2-substituted phenylboronic acids are 2-carboxy and 2- alkoxycarbonyl phenylboronic acids, where the alkoxy group has 1-3 carbon atoms.
  • the additional substituents of the substituted phenylboronic acids are one or more electron withdrawing groups.
  • additional substituents are selected from the group consisting of halogen, nitro, cyano, an alkyl group, an alkoxy group, an alkoxycarbonyl group, a carboxyalkyl group, an alkoxycarbonylalkyl group, an aminoalkyl group, an alkylaminoalkyl group, -COH, -COR 7 , -C0 2 H, -C0 2 R 8 , -NH 2 , -CONH 2 , -N(R 9 ) 2 , or - CON(Rci) 2i where R 7 , Rs and each R 9 is independently selected from an alkyl group, an aralkyl group or an aryl group. Alkyl, alkoxy, aralkyl and aryl groups of the substituents herein are optionally substituted as defined herein.
  • Preferred alkyl and alkoxy substituents have 1-3 carbon atoms.
  • Preferred R 7 and Rs of substituents herein are hydrogen, alkyl having 1-3 carbons, phenyl and benzyl groups.
  • alkyl, alkoxy, aralkyl and aryl groups of substituents herein are unsubstituted.
  • alkyl aralkyl and aryl groups are substituted with one or more halogens.
  • haloalkyl groups are perfluoroalkyl groups, particularly those having 1-3 carbon atoms.
  • halogen substituents are F, CI or Br and in more specific embodiments, halogens are chlorines.
  • the substituted phenylboronic acid is a carboxy or alkoxycarbonyl substituted phenylboronic acid, particularly a phenylboronic acid substituted with a 2-carboxy, a 2-methoxycarbonyl or a 2-ethoxycarbonyl group and optionally further substituted as noted above.
  • substituents for 2-carboxy, a 2-methoxycarbonyl or a 2- ethoxycarbonyl phenylboronic acids are selected from the group consisting of methyl, ethyl, methoxy, ethoxy, chloro, fluoro, cyano, nitro, trifluoromethyl, formyl, acetyl, -NH 2 , -CONH 2 , and N,N-dimethylaminomethyl.
  • the carbohydrate is contacted at a selected temperature with the phenylboronic acid alone or in combination with an anhydrous or hydrated magnesium or calcium halide salt, particularly an anhydrous or hydrated magnesium or calcium chloride in an appropriate solvent.
  • the phenylboronic acid is optionally in the form of a hydrate or a salt.
  • addition of selected amounts of water to the reaction can enhance the yield of desired furan products. Reaction is typically continued to obtain a desired yield of furan(s). It is preferred to maximize the yield of furans (i.e., HMF and/or furfural) and minimize undesirable side-products, for example, from degradation or polymerization of the desired furan products.
  • the invention provides methods for producing HMF from ketohexose, particularly glucose, and aldohexoses, particularly galactose, in the presence of certain substituted phenylboronic acids, particularly those carrying a 2-methoxycarbonyl or a 2- ethoxycarbonyl group.
  • the phenylboronic acids may carry one to four or one or two additional substituents as noted above.
  • no metal salt is required for production of HMF.
  • an anhydrous or hydrated magnesium and calcium chloride can enhance the yield of HMF.
  • the addition of water to the reaction can enhance the yield of HMF.
  • mono- and disaccharides are converted to the furans, HMF and/ or furfural, in the presence of certain 2-substituted phenylboronic acids, and a hydrated magnesium or calcium halide salt in polar aprotic solvent other than an ionic liquid, an ionic liquid or mixtures thereof.
  • mono- and disaccharides are converted to HMF and/ or furfural, in the presence of certain phenylboronic acids, and a hydrated magnesium or calcium halide salt in an ionic liquid.
  • the furan is HMF.
  • the furan is furfural.
  • a mixture of HMF and furfural is generated.
  • the invention provides methods for producing HMF from glucose in a dipolar aprotic solvent other than an ionic liquid in the presence of certain substituted phenylboronic acids, particularly 2-carboxy-substituted phenylboronic acids, 2- methoxycarbonyl-substituted phenylboronic acids, 2-ethoxycarbonyl-substituted phenylboronic acids, or 3-carboxy-5-nitrophenylboronic acid.
  • no metal salt is required to produce HMF.
  • an anhydrous or hydrated magnesium or calcium chloride can enhance the yield of HMF.
  • the addition of water to the reaction can enhance the yield of HMF.
  • hexose oligomers, pentose oligomers and mixtures thereof are converted to furans at high yields by reaction with certain 2-substituted phenylboronic acids in a dipolar aprotic solvent other than an ionic liquid in the absence of magnesium or calcium salt and in the absence of added water.
  • a dipolar aprotic solvent other than an ionic liquid in the absence of magnesium or calcium salt and in the absence of added water.
  • Addition of anhydrous or hydrated magnesium or calcium halide can enhance the production of furans.
  • Addition of a selected amount of water can enhance the production of furans.
  • glucose oligomers such as cellobiose, cellotriose, or cellotetrose
  • a dipolar aprotic solvent other than an ionic liquid e.g., DMA
  • anhydrous or hydrated magnesium or calcium halide can enhance the production of furans.
  • Addition of a selected amount of water can enhance the production of furans.
  • cellulose, hemicellulose, or lignocellulosic biomass is converted to furans in the presence of certain 2-substituted phenylboronic acids, and dilute mineral or organic acid (other than a boronic acid) in ionic liquid or a mixture of ionic liquid and a dipolar aprotic solvent other than an ionic liquid (e.g., DMA).
  • ionic liquid or a mixture of ionic liquid and a dipolar aprotic solvent other than an ionic liquid e.g., DMA
  • an anhydrous or hydrated magnesium or calcium halide is added to enhance production of furans. Addition of a selected amount of water can enhance production of furans.
  • the present invention also provides a method for producing fructose by reacting glucose or glucose oligomers in the presence of certain 2-substituted phenylboronic acids and magnesium oxide in a dipolar aprotic solvent other than an ionic liquid, an ionic liquid or mixtures thereof.
  • the methods of the invention employ 2-substituted phenylboronic acids which are immobilized on a solid substrate, such as a substrate surface or a resin.
  • the 2-substituted phenylboronic acids are immobilized to the surface by covalent attachment by a linker moiety to the surface or resin.
  • covalent attachment can be to the 4- or 5-ring position of the phenyl ring of the 2-substituted
  • phenylboronic acid The use of immobilized phenylboronic acids facilitates their recycling and reuse and facilitates product recovery and purification.
  • the invention provides catalyst compositions for formation of furans from carbohydrates, including mono- and disaccharides, cellulose and other polymers and
  • Catalyst compositions comprise one or more 2-substituted
  • catalyst compositions comprise one or more 2-substituted phenylboronic acids immobilized on a solid, such as a substrate surface or a resin.
  • catalyst compositions comprise one or more 2-substituted phenylboronic acids in combination with a magnesium or calcium chloride salt or mixture of such halide salts.
  • the magnesium or calcium halide salt is hydrated.
  • the halide salt is MgCl 2 .
  • the salt is MgCl 2 -6H 2 0.
  • the substituted phenylboronic acids are those carrying a 2-nitro, 2-alkyl, 2-alkoxy, 2-haloalkyl, a 2-aminocarbonyl, a 2-, 3-, 4- or 5-haloalkyl group, a 2-, 3- or 4-carboxy or a 2-, 3-, or 4-alkoxycarbonyl group.
  • the substituted phenylboronic acids of the compositions are 2-substituted phenylboronic acids.
  • the substituted phenylboronic acids as described above can in addition carry one to four and more preferably one or two, additional substitutents as defined below.
  • the phenylboronic acid is optionally in the form of a hydrate (e.g., a monohydrate) or a salt.
  • Preferred 2-substituted phenylboronic acids are 2-carboxy and 2-alkoxycarbonyl phenylboronic acids, where the alkoxy group has 1-3 carbon atoms.
  • the invention further provides a carbohydrate dehydration medium which comprises a catalyst composition for formation of HMF as provided herein in ionic liquid, a polar aprotic solvent other than an ionic liquid or a mixture thereof.
  • the carbohydrate dehydration medium contains a selected amount of water.
  • the carbohydrate dehydration medium can comprise an acid other than a phenylboronic acid.
  • the carbohydrate dehydration medium comprises dilute organic or mineral acid.
  • 2-substituted phenylboronic acids useful in the methods and catalyst compositions of this invention are those of formula I:
  • R is selected from an alkyl group, a hydrogen, an aralkyl group, or an aryl group, each of which is optionally substituted;
  • P 3-R ⁇ 5 independently, are selected from hydrogen, halogen, nitro, cyano, an alkyl group, an alkoxy group, an alkoxycarbonyl group, a carboxyalkyl group, an alkoxycarbonylalkyl group, an aminoalkyl group, an alkylaminoalkyl group, -COH, -COR 7 , -C0 2 R 8 -NH 2 , -COM 2 , -N(R 9 ) 2 , or -CON(Rci) 2i where R 7 , Rs and each R 9 is independently selected from an alkyl group, an aralkyl group or an aryl group. Alkyl, alkoxy, aralkyl and aryl groups of the substituents herein are optionally substituted. Preferred alkyl and alkoxy substituents are have 1-3 carbon atoms.
  • R 7 and Rs of substituents herein are hydrogen, alkyl having 1-3 carbons, phenyl and benzyl groups.
  • alkyl, alkoxy, aralkyl and aryl groups of substituents herein are unsubstituted.
  • haloalkyl groups are perfiuoroalkyl groups, particularly those having 1-3 carbon atoms.
  • halogen substituents are F, CI or Br and in more specific embodiments, halogens are chlorines.
  • one of R 3 -R 6 is (1) a linker group covalently attached to a surface, (2) a linker group suitable for attachment of the phenylboronic acid to a surface or (3) a reactive group with optional linker suitable for forming a covalent attachment to a surface directly or through a linker.
  • alkyl, alkoxy, aralkyl, aryl and other groups in the definitions herein are optionally substituted with one or more halogen, hydroxyl, nitro, cyano, alkyl, haloalkyl, aryl, amine, alkoxy, -COOR10, -COR10, -SR 10 , or -CO-N(Rio) groups, where Rio is hydrogen or an alkyl, araalkyl or aryl group.
  • substituents for optional substitution are one or more halogen, one or more alkyl having 1-3 carbon atoms, an amine, an alkoxy having 1-3 carbon atoms, a trifluoromethyl group, -COOH, -COOCH 3 , or -COOC 2 H 5 .
  • R is hydrogen or an unsubstituted alkyl group having 1-3 carbon atoms.
  • alkyl and alkoxy groups have 1-3 carbon atoms.
  • alkyl, alkoxy, aralkyl and aryl groups are unsubstituted.
  • alkyl, alkoxy, aralkyl and aryl groups are substituted. More specifically, alkyl, alkoxy, aralkyl, or aryl groups are substituted with one or two non-hydrogen substituents.
  • substituted alkyl groups, aryl groups, aralkyl, benzyl or phenyl groups are substituted with one or more halogens.
  • R is hydrogen or an alkyl group having 1-3 carbon atoms.
  • Phenylboronic acids may be in the form of salts with an appropriate anion or cation.
  • Phenylboronic acids may be in the form of hydrates, particularly monohydrates.
  • R, R 7 or R 8 which are aryl groups are phenyl groups. In specific embodiments, R, R 7 or Rs which are aralkyl groups are benzyl groups.
  • R 3 -R 6 are all hydrogens, one or two of R3-R6 are alkyl and the remainder are hydrogen, one or two of R 3 -R 6 are halogens and the remainder are hydrogen, one or two of R 3 -R 6 are alkoxy and the remainder are hydrogens, one or two of R3-R6 are halogenated alkyl groups and the remainder are hydrogen, one or two of R 3 -R 6 are halogenated alkoxy groups and the remainder are hydrogens, one or two of R 3 -R 6 are nitro groups and the remainder are hydrogens.
  • the invention also relates to methods for making useful derivatives and products of HMF such as 2,5-furandicarboxylic acid, 2,5-bis(hydroxymethyl)furan, 2,5-bis(hydroxymethyl)
  • dipolar aprotic solvents other than ionic liquids are DMA and N-methylpyrrolidone.
  • ionic liquids having chlorine anions can be employed.
  • the ionic liquid is an alkylimidazolium ionic liquid or an
  • the alkylpyridinium ionic liquid is [EMIMJCl (1- ethyl-3-methylimidazolium chloride), [BMIMJC1 (l-butyl-3-methyl-imidazolium chloride), 1- ethyl-2,3-dimethylimidazolium chloride, or l-butyl-4-methylpyridinium chloride or mixtures thereof.
  • reactions of the invention are conducted at temperatures ranging from about 100 to 150 °C, more specifically from 100 to 130 °C or from 105 to 130 °C.
  • Fig. 1 provides Scheme 1 which schematically illustrates production of HMF from cellulose by hydrolysis (I) to generate glucose, isomerization of glucose (II) to fructose and dehydration of fructose (III).
  • Fig. 3 provides Scheme 3 which illustrates various art-known conversions of HMF to produce fuels and commercially important chemical starting materials.
  • the scheme also illustrates the possible production of undesired side products from fructose or HMF.
  • Undesired side products include products of polymerization, which include insoluble materials designated humins.
  • Fig. 6 provides Scheme 6 which illustrates an alternative method for immobilization of 2- substitued phenylboronic acids.
  • This scheme schematically illustrates protection of the phenylboronic acid in the form of a protected oxaborole and formation of an exemplary activated ester of the protected oxaborole. The activated ester is then reacted with a surface-bound amine group to immobilize the oxaborole which can be deprotected when desired.
  • Fig. 8 illustrates an exemplary phenylboronic catalyst recovery and recycling process which is described in Example 7.
  • Schemes 1 and 2 (FIGS 1 and 2) illustrate generation of furans from carbohydrates.
  • carbohydrates or lignocellulosic biomass is contacted with the 2-substituted phenylboronic acid salt (or hydrate) and a magnesium or calcium salt (or hydrate thereof) in an ionic liquid, a polar aprotic solvent other than an ionic liquid or a mixture thereof.
  • Water can be present in the reaction either added in hydrated reaction components, present in the substrate carbohydrate or biomass or as added to the reaction. The presence of selected amounts of water can enhance furan production.
  • Dilute acid (other than a phenylboronic acid), particularly mineral acid, is added to facilitate hydrolysis of carbohydrate polymers when necessary.
  • reactions are conducted at temperatures ranging from about 100 to 150 °C, more specifically from 100 to 130 °C and yet more specifically from about 105 to 130 °C. It will be appreciated that it can be preferred to run a reaction at the lowest temperature that will provide a desired product yield to decrease energy costs. Typically reactions are run at ambient pressure, but can be conducted at elevated pressures.
  • the salt is a magnesium salt. In other specific embodiments, the salt is a calcium salt. In specific embodiments, the salt is magnesium halide or calcium halide. In specific embodiments, the salt is magnesium chloride or calcium chloride. Mixtures of such salts can be employed. In specific embodiments, the salt is hydrated magnesium chloride. In specific embodiments, no Li is added to or present in the reaction medium. In specific embodiments, no LiCl is added to the reaction. In specific embodiments, no metal salts other than magnesium and/or calcium chloride salts are added to or present in the reaction medium.
  • magnesium(II) and/or calcium(II) is present in the reaction in a total amount greater than 10 mol% with respect to the carbohydrate substrate.
  • magnesium(II) or calcium(II) or a mixture thereof is present in the reaction in a total amount of 100 mol% to 500 mol% with respect to the carbohydrate substrate. In specific embodiments, magnesium(II) or calcium(II) or a mixture thereof is present in the reaction in a total amount of 100 mol% to 300 mol%.
  • the molar ratio of phenylboronic acid to magnesium(II) and/or calcium(II) or a mixture thereof in the reaction, in catalyst compositions or in carbohydrate dehydration medium is 0.5 to 5. In other embodiments, the molar ratio of phenylboronic acid to magnesium(II) or calcium(II) or a mixture thereof is 1 to 3. In other embodiments, the molar ratio of phenylboronic acid to magnesium(II) or calcium(II) or a mixture thereof is 2.
  • the phenylboronic acids employed in the reactions herein bind to sugars facilitating the conversions and preventing at least in part the undesired polymerization of sugars.
  • the phenylboronic acids are believed to act as catalysts or promoters which can be recovered from the reaction mixtures.
  • the ability to recover phenylboronic acids for recycling and reuse can result in decreased costs for carrying out conversions of this invention.
  • Recovery and recycling of phenyboronic acids can be facilitated by immobilizing the phenylboronic acid on a solid.
  • An exemplary catalyst recycling and recovery process is provided in Example 7 and illustrates in FIG. 8. This process also provides for recovery of product furan.
  • Reaction can be carried out in a batch mode or a continuous or semi-continuous mode. Reaction is carried out until a desired level of product is formed. In batch mode, the exact length of reaction will be dependent upon the temperature, concentration of reagents and the amount and type of substrate (carbohydrate/biomass). In specific embodiments, reactions are carried out for 0.5-24 hours, more preferably for 1-10 hours and yet more preferably in 1-4 hours. The length of time the reaction is run can be optimized by assessing product yield as a function of reaction time for a given set of reaction conditions. Catalyst and salt concentration and the amount of water can be varied to achieve desired yields. In continuous or semi-continuous mode, products are periodically removed from the reaction.
  • Fig. 8 illustrates an exemplary product recovery process.
  • Substrate loading (the amount of substrate to solvent in a reaction) can vary dependent upon the substrate and reactor in which the reaction is carried out. In specific embodiments, where the substrate is glucose or an oligomer thereof, substrate loading can range up to 20 wt%, including 5-15 wt%. In specific embodiments, where the substrate is cellulose or lignocellulosic biomass, substrate loading can range up to 10 wt%, including 2-6 wt%.
  • substrate loading can range up to 10 wt%, including 2-6 wt%.
  • water present in the substrate in any hydrated reagents and in solvents, should be considered.
  • the total water present in the reaction ranges from 1-25 molar equivalents with respect to substrate or monomer content of substrate. More specifically, improved yield has been observed in certain cases where 1-6, 6 or more, 6-12 or 12 or more equivalents of water with respect to glucose are present. It is noted that it might be expected that increased water concentrations would inhibit dehydration reactions, however, the presence of selected amounts of water increases the yield of HMF and furfural.
  • FIG. 7 is a graph showing the dependence of HMF yield from glucose on the molar ratio of H 2 0 to Mg[II]. Yield increases as this ration increases, but begins to level off when the ratio is high than 6.
  • the molar ratio of H 2 0 to Mg or Ca can range from 0.5 to 10, more preferably is 1-10, and yet more preferably is 5- 10.
  • the molar ratio of H 2 0 to Mg or Ca is 3 or higher, 5 or higher or 6 or higher.
  • the invention provides a method for making fructose from glucose, glucose oligomers or a mixture thereof which comprises heating these carbohydrates in the presence of certain 2-substituted phenylboronic acids and magnesium oxide in a dipolar aprotic solvent other than an ionic liquid, an ionic liquid or a mixture thereof to form a reaction mixture.
  • glucose is converted to fructose.
  • MgO is added at a level ranging from 50 to 500 mol% and more specifically from 100 to 300 mol% with respect to glucose present in the substrate. No water needs to be added to the reaction.
  • the reaction mixture is heated to 100-150 °C or more specifically to 105 to 130 °C.
  • the phenylboronic acid is present in the reaction at levels ranging from 10 mol% to 300 mol% or more preferably at levels from 60 mol% to 100 mol% with respect to substrate.
  • salt is present in the reaction at levels ranging from 50 mol% to 1000 mol%, or more preferably at levels from 150 mol% to 500 mol%, and yet more preferably at levels from 150 to 300 mol% with respect to substrate.
  • the salt is present in the reaction at levels ranging from 50 mol% to 1000 mol% with respect to substrate. Where the substrate is a monosaccharide, mol% is measured with respect to the substrate itself.
  • the substrate is an oligo- or polysaccharide (e.g., cellulose)
  • mol% is measured with respect to monomer in the oligomer or polysaccharide.
  • the substrate is biomass, mol% is measured with respect to monomer in the cellulose or hemicellulose present in biomass.
  • the phenylboronic acid is immobilized on a solid surface and the surface carrying the phenylboronic acid is contacted with the reaction mixture
  • the solid surface can be that of any material that is compatible with the chemistry of the reactions herein.
  • the surface and the linker from the surface to the phenylboronic acid should be stable to the conditions of the reactions herein, for example, the phenylboronic acid should substantially remain immobilized, e.g., covalently attached, to the surface during the course of the reaction.
  • Surfaces that can be used in this invention include, but are not limited to glass (including glass slides), quartz (including optical fibers), various metal surfaces such as gold, including gold with thiol monolayers, colloidal gold, semiconductors, diamond, silicon, plastic, ceramics, alum, hydroxyapatite, polyacrylamide, polyimines, polypropylene, latex, rubber, agarose, chitin, chitosan, dextran and derivatized dextrans, cellulose and derivatized cellulose (e.g., nitrocellulose, cellulose acetate), nylon, polyvinyl chloride, and polystyrene (resins, etc.), artificial bone material.
  • glass including glass slides
  • quartz including optical fibers
  • various metal surfaces such as gold, including gold with thiol monolayers, colloidal gold, semiconductors, diamond, silicon, plastic, ceramics, alum, hydroxyapatite, polyacrylamide, polyimines, polypropylene, latex, rubber, agarose
  • Surfaces can be multilayered, e.g., glass surfaces with deposited metal surfaces, e.g., deposited gold, with optional polymer coatings (e.g., carboxymethylated dextran) as exemplified by BIACORE® sensor chips (Trademark, Biacore AB).
  • Surfaces can be flat or curved and can be a film, a plate, a fiber, plate wells, a wafer, a grid, a mesh, a membrane, beads or pins.
  • Surfaces can be rigid or pliable, or the surface of a gel. Surfaces may further be composed of a plurality of solid particles, microspheres, resins or beads.
  • Resins carrying reactive groups useful for immobilization of phenylboronates include, among others, Wang resins, TentaGelTM resins, PEG resins, polystyrene resins, StratospheresTM, JandajelTM resins and Novabiochem® resins (e.g., Amino PEGA resin, NovaPEG amino resin, Nova Syn® TG amino resin, Nova Syn® TG carboxy resin, Carboxypolystyrene HL resin).
  • phenylboronic acids are immobilized onto a surface via a linker.
  • the surface is derivatized to carry chemically reactive groups which may be spaced from the surface by linker moieties to which the reactive groups are covalently bonded. These surface bound reactive groups react with a chemically compatible reactive group of the phenylboronate to form a covalent bond.
  • the phenylboronate is attached to the surface such that it remains active for promoting the reactions herein.
  • attachment of the phenylboronate to the surface is preferably via a reactive group substituent on the phenyl ring other than the 2-position.
  • attachment of the phenylboronate to the surface is preferably via a reactive group substituent on the 3- or 4-position of the phenyl ring.
  • the reactive group can be an activated ester group, such as an N-hydroxysuccinimide ester group.
  • a reactive group is substituted onto the phenylboronate via an intermediate linker moiety.
  • a reactive group suitable for reacting with a surface or a derivatized surface e.g., a derivatized resin, including, e.g., a Wang resin
  • a surface or a derivatized surface is generated on the linker moiety such that the reactive group is spaced from the phenylboronate by the linker moiety.
  • the reactive group and intermediate linker are attached to the /?ara-position of the phenyl ring of the phenylboronate.
  • a linker moiety from a surface to the phenylboronate can be schematically illustrated as:
  • phenylboronate LI and L2 and L3 are optional linker moieties and Ml, M2, M3, and M4 are optional bonds formed from reaction of reactive groups. At least one of L1-L3 and one of Ml-
  • M4 are present. Any linear or branched linker moiety can be employed. In specific
  • various supports with Ml, LI, M2 and/or L2 in place or with reactive groups to form Ml, M2 or M3 are commercially available which can be used for immobilization of phenylboronates which can be provided with one or more appropriate linkers (e.g., L2 and/or L3) or reactive groups to form M3/M4.
  • linker moieties can be from 4-100 bonds in length or more specifically 6-20 bonds in length.
  • arylene linkers such as 1,4- arylene linkers can be employed, optionally in combination with alkylene linkers.
  • linkers include 1 ,4-phenylene or l,4'-biphenylene groups.
  • phenylboronates can be linked to surfaces via polyethylene glycol (PEG) linkers. Additionally, phenylboronates can be linked to surfaces via -Yl-(CH 2 ) m -Y2 moieties where Yl and Y2 are independently selected from -0-, -S-, -0-CO-, -OC-0-, -CO-, -NR15-, -N-CO-, or -CO-N-, where R15 is hydrogen and alkyl or an aryl group. Phenylboronates can be substituted with reactive groups suitable for reaction with linkers for attachment to surfaces.
  • PEG polyethylene glycol
  • Such reactive groups include vinyl groups, esters, active esters, N-hydroxysuccinimide esters, amides, amines, azides, hydrazines, alcohols, aldehydes, amines, amides, and alkyl halide groups, among others.
  • surfaces can be derivatized or substituted with reactive groups, such as those listed above, for reactions with linkers covalently attached to
  • phenylboronates or for reaction with groups on the phenylboronates.
  • any chemical linkage system known in the art for attaching a chemical or biochemical species to a surface and that is compatible with the application of the phenylboronates in reactions of this invention can be used to attached phenylboronates of this invention to a surface.
  • Useful 2-substituted phenylboronic acids are commercially available, or can be prepared in view of the descriptions herein and what is known to one of ordinary skill in the art from readily available starting materials by methods that are well known in the art or by routine adaptation of such well-known methods. Synthesis of useful phenylboronic acids are described, for example, in: B. Tao, S. C. Goel, J. Singh and D. W. Boykin (2002). A practical preparation of 2- carboxyphenylboronic acid and its application for the preparation of biaryl-2-carboxylic acids using Suzuki coupling reactions Synthesis, 8: 1043-1046; and D.G.
  • 2-carboxy and 2-alkoxycarbonylphenylboronic acids can also be prepared from corresponding oxaboroles by methods that are well-known in the art.
  • Oxaboroles are commercially available or can be prepared by methods that are well-known in the art. Methods for preparation of various ring substituted oxaboroles are provided, for example, in U.S. patents 5,880,198;
  • Phenylboronic acids can be in the form of hydrates, particularly monohydrates, which can be prepared, for example by recrystallization methods that are known in the art.
  • phenylboronic acid hydrates are commercially available.
  • the hydrate form of certain phenylboronic acids may exhibit enhanced shelf-life.
  • alkyl refers to a monoradical of a branched or unbranched (straight-chain or linear) saturated hydrocarbon and to cycloalkyl groups having one or more rings. Unless otherwise indicated alkyl groups have 1 to 22 carbon atoms, 1-12 carbon atoms or 1-6 carbon atoms. Alkyl groups include methyl, ethyl, propyl, butyl, pentyl and hexyl groups, including all isomers thereof. Alkyl groups can be straight-chain, branched or cyclic.
  • cycloalkyl refers to cyclic alkyl groups having 3 to 22 and 3-6 carbon atoms having a single cyclic ring or multiple condensed rings.
  • Cycloalkyl groups include, by way of example, single ring structures such as cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cyclooctyl, and the like, or multiple ring structures such as adamantanyl, and the like. Unless otherwise indicated alkyl groups including cycloalkyl groups are optionally substituted as defined herein.
  • the term "aralkyl” refers to an alkyl group substituted with an aryl group (i.e., arylated alkyl), exemplary aralkyl groups are optionally substituted benzyl groups.
  • Carboxyalkyl group refers to an alkyl group substituted with a -C0 2 H or -C0 2 " moiety, such as -(CH 2 )n-C0 2 H, where n is 1-6 or 1-3.
  • Carboxy moieties may be in the form of carboxylate salts with various cations.
  • Alkoxycarbonylalkyl group refers to an alkyl group substituted with a -CO-O-R', where R' is alkyl, such as -(CH 2 ) n -CO-0-(CH 2 ) m H, where n and m are independently integers from 1-6 or 1-3.
  • Aminoalkyl group refers to an alkyl group substituted with one or more -NH 2 groups, preferably one -NH 2 group, such as -(CH 2 ) n -NH 2 , where n is 1-6 or 1-3.
  • alkoxy refers to the group -OR where R is an alkyl group as defined above. In specific embodiments , alkoxy groups have 1-6 carbons atoms or 1-3 carbon atoms.
  • alkoxycarbonyl refers to a -C0 2 R group where R is an alkyl group where in specific embodiments, R is an alkyl group having 1-6 or 1-3 carbon atoms.
  • aryl refers to a monoradical containing at least one aromatic ring.
  • the radical is formally derived by removing a H from a ring carbon.
  • Aryl groups contain one or more rings at least one of which is aromatic. Rings of aryl groups may be linked by a single bond or a linker group or may be fused. Exemplary aryl groups include phenyl, biphenyl and naphthyl groups.
  • Aryl groups include those having from 6 to 30 carbon atoms and those containing 6-12 carbon atoms. Unless otherwise noted aryl groups are optionally substituted as described herein.
  • Aryl groups include optionally substituted phenyl groups.
  • activated ester refers to an ester group -CO-OY where -OY is a good leaving group.
  • a good leaving group typically is an organic group which can stabilize a negative charge including aliphatic and aryl groups substituted with at least one electron withdrawing group.
  • activated esters react with amines to form amides.
  • Useful -OY groups for activated esters include, among others:
  • -O-aryl groups particularly those substituted with one or more electron withdrawing groups, e.g., halide, nitro group, cyano group, or trifiuoromethyl group, and more particularly -O-phenyl groups substituted with one or more electron withdrawing groups; or
  • N-oxy heterocycles including N-oxysuccinimdyl, N-oxyphthalimide, or 1-oxybenzotriazolyl:
  • optional substitution means substitution by one or more non- hydrogen substituents selected from halogen, hydroxyl, amine, cyano, azide, nitro, isocyanate, isothiocyanate, C1-C6 alkyl, C1-C3 alkyl, C1-C6 haloalkyl, C1-C3 haloalkyl, phenyl, benzyl, sulfate, phosphate, phosphonate, carboxyl, sulfonyl, sulfonamide, and amide. All alkyl, aralkyl, or aryl groups herein are optionally substituted with one or more non-hydrogen substituents unless otherwise specified.
  • Substitution may be on one or more carbons or, if feasible, on one or more heteroatoms, e.g., a nitrogen.
  • the number of substituents on such groups depends generally upon the nature of the group, but includes substitution with one, two, three, four, five or six substituents.
  • the compounds of this invention may contain one or more chiral centers. Accordingly, this invention is intended to include racemic mixtures, diasteromers, enantiomers and mixture enriched in one or more stereoisomer.
  • the scope of the invention as described and claimed encompasses the racemic forms of the compounds as well as the individual enantiomers and non- racemic mixtures thereof.
  • salts may form salts which are also within the scope of this invention.
  • Reference to a compound of the formulas herein is understood to include reference to salts thereof, unless otherwise indicated.
  • a compound of a formula herein contains both a basic moiety, such as, but not limited to an amine and an acidic moiety, such as, but not limited to, a carboxylic acid
  • zwitterions inner salts
  • Salts should be compatible with reaction conditions used in the methods herein. Salts of compounds herein may be formed, for example, by reacting the compound with an amount of acid or base, such as an equivalent amount, in a medium such as one in which the salt precipitates or in an aqueous medium followed by lyophilization.
  • Exemplary acid addition salts include acetates (such as those formed with acetic acid or trihaloacetic acid, for example, trifluoroacetic acid), adipates, alginates, ascorbates, aspartates, benzoates, benzenesulfonates, bisulfates, borates, butyrates, citrates, camphorates,
  • camphorsulfonates cyclopentanepropionates, digluconates, dodecylsulfates, ethanesulfonates, fumarates, glucoheptanoates, glycerophosphates, hemisulfates, heptanoates, hexanoates, hydrochlorides (formed with hydrochloric acid), hydrobromides (formed with hydrogen bromide), hydroiodides, 2-hydroxyethanesulfonates, lactates, maleates (formed with maleic acid), methanesulfonates (formed with methanesulfonic acid), 2-naphthalenesulfonates, nicotinates, nitrates, oxalates, pectinates, persulfates, 3-phenylpropionates, phosphates, picrates, pivalates, propionates, salicylates, succinates, sulfates (such as those formed with sulfuric
  • Exemplary basic salts include ammonium salts, alkali metal salts such as sodium, lithium, and potassium salts, alkaline earth metal salts such as calcium and magnesium salts, salts with organic bases (for example, organic amines) such as benzathines, dicyclohexylamines, hydrabamines [formed with N,N-bis(dehydro-abietyl)ethylenediamine], N-methyl-D-glucamines, N-methyl-D-glucamides, t-butyl amines, and salts with amino acids such as arginine, lysine and the like.
  • organic bases for example, organic amines
  • organic bases for example, organic amines
  • benzathines dicyclohexylamines
  • hydrabamines [formed with N,N-bis(dehydro-abietyl)ethylenediamine]
  • N-methyl-D-glucamines N-methyl-D-glucamides
  • any one of the isomers or a mixture of more than one isomer is intended.
  • the compounds useful herein may be in the free or hydrate form.
  • Dipolar aprotic solvents other than ionic liquids, certain ionic liquids and mixtures thereof, particularly miscible mixtures thereof, can be employed as solvents herein for carbohydrates and biomass and for the conversion of such materials to one or more furans.
  • Lignocellulosic materials need not be soluble in these solvents. Such materials may be decrystallized, swollen, partially solubilized or structurally disrupted by contact with the solvents herein.
  • dipolar aprotic solvent refers to solvents other than ionic liquids which have a dielectric constant of greater than about 15, a sizeable permanent dipole moment and that cannot donate suitably labile hydrogen atoms to form strong hydrogen bonds [See: "GLOSSARY OF TERMS USED IN PHYSICAL ORGANIC CHEMISTRY", IUPAC Recommendations 1994, P. Miiller, Pure Appl. Chem., 66, 1077-1184 (1994)].
  • Dipolar aprotic solvents are also commonly called polar aprotic solvents in the art.
  • Dipolar aprotic solvents which are not ionic liquids, include among others N,N-dialkylacetamides, N,N-dialkylformamides, 2-pyrrolidones or 3- pyrrolidones (including alkyl- or N-alkyl-substituted pyrrolidinones), pyrolidine
  • alkyl groups are preferably those having 1-6 carbon atoms or those having 1-3 carbon atoms and wherein the alkyl groups may be straight-chain, branched or cyclic.
  • Useful solvents include among others, N,N-dimethylacetamide (DMA), N,N-diethylacetamide (DEA), dimethylformamide (DMF), N-methylpyrrolidone, l-ethyl-2-pyrrolidinone,
  • Preferred solvents include DMA and N- methylpyrrolidone.
  • Additional polar aprotic solvents include acetone, and other ketones, nitroalkanes, such as nitromethane and nitroethane, hexamethylphosphoramide, and
  • hexamethylphosphorous triamide hexamethylphosphorous triamide.
  • Acetone and other ketones are less preferred for use in this reaction because of potential formation of ketals (from ketones) with sugar hydroxyl groups.
  • Nitroalkanes are less preferred for use in this reaction because of potential side reactions with saccharides or furan products.
  • reactions of this invention are conducted using ionic liquid or mixtures of ionic liquid with a polar aprotic solvent other than an ionic liquid.
  • An ionic liquid is a salt that melts near or below ambient room temperature.
  • the ionic liquid is liquid at the reaction temperature.
  • the ionic liquid is one in which cellulose is soluble to some measurable extent.
  • the ionic liquid is one in which up to about 5-25 weight% or more cellulose is soluble. More preferably the ionic liquid is one in which up to about 25 weight% or more cellulose is soluble.
  • a number of ionic liquids have been shown in the art to dissolve cellulose.
  • the cation of the ionic liquid is an organic cation, particularly a cation containing at least one positively charged nitrogen atom.
  • the ionic liquid is an alkylimidazolium ionic liquid, more particularly an alkylimidazolium halide or an alkylimidazolium acetate, and yet more particularly an alkylimidazolium chloride ionic liquid.
  • the ionic liquid is a 1,3-dialkylimidazolium chloride, a 1,3- dialkylimidazolium acetate, a 1,2,3-trialkylimidazolium chloride or a 1,2,3-trialkylimidazolium acetate.
  • the ionic liquid is [EMIMJCl (l-ethyl-3- methylimidazolium chloride), [BMIMJC1 (l-butyl-3-methyl-imidazolium chloride), or 1-ethyl- 2,3-dimethylimidazolium chloride, or a mixture thereof.
  • the ionic liquid is l-ethyl-3-methylimidazolium acetate), l-butyl-3 -methyl -imidazolium acetate or 1- ethyl-2,3-dimethylimidazolium acetate, or a mixture thereof.
  • the ionic liquid is an alkylpyridinium ionic liquid, particularly an alkyl pyridinium halide or an
  • the ionic liquid is a 1 -alkylpyridinium ionic liquid, a 1,4- dialkylpyridinium chloride or a 1 ,4-dialkylpyridinium acetate.
  • the ionic liquid is 1-ethylpyridinium acetate, l-butyl-4-methylpyridinium acetate, or a mixture thereof.
  • the ionic liquid is 1-ethylpyridinium chloride, 1 -butyl -4- methylpyridinium chloride, or a mixture thereof.
  • Additional ionic liquids useful in the invention particularly those in which chloride or acetate is the anion of the salt of the ionic liquid, are provided in US 2008/0033187. Additional organic cations of ionic liquids are described in US 2009/0062524, WO2009030950, WO2009030849, US20090020112, WO2008112291, US20080227162 and WO2009024607, each of which is incorporated by reference herein for descriptions of such cations.
  • Ionic liquids may be characterized by either the anion or cation of the salt.
  • chloride-containing ionic liquid refers to an ionic liquid in which the anion of the salt is chloride; analogous terms may be used for ionic liquids containing other anions, such as
  • the term "alkylimidazolium-containing ionic liquid” and similar terms reciting the cations of ionic liquids refer to an ionic liquid wherein the cation has the structure named.
  • the ionic liquid is a chloride-containing ionic liquid It is believed that the acidity of ionic liquids can vary from batch to batch and as a function of the source (e.g., the manufacturer of a given commercial ionic liquid or the method of synthesis employed to prepare the ionic liquid compound).
  • the amount of acid may vary dependent upon the methods employed to make or to purify the ionic liquid.
  • ionic liquids that are sufficiently contaminated with acid may not require addition of acid catalyst or may require addition of lower levels of acid catalyst than are described herein.
  • One of ordinary skill in the art will recognize that there are well-known methods for assessing acidity which can be applied to assessing the acidity of ionic liquids prior to their use in the methods of this invention.
  • One method that is applicable is a standard acid-base titration.
  • methods are known in the art for decreasing acidity of an ionic liquid which can be applied if desired.
  • the ionic liquid is an alkylimidazolium ionic liquid, more particularly an alkylimidazolium halide ionic liquid. In other specific embodiments, the ionic liquid is an alkylimidazolium chloride ionic liquid. In more specific embodiments, the ionic liquid is
  • the ionic liquid is an alkylpyridinium ionic liquid, more particularly an alkylpyridinium halide ionic liquid.
  • the ionic liquid is 1-ethylpyridinium chloride, 1 -butyl -4-methylpyridinium chloride, or a mixture thereof. Additional ionic liquids useful in this invention are provided in US 2008/0033187.
  • the amount of ionic liquid added ranges from 5 wt % to 95 wt% or from 10 wt% to 50 wt%. In other embodiments, the amount of ionic liquid is 95 wt% or more. In other
  • the amount of ionic liquid is 50 wt% or less, 30 wt% or less, 25 wt% or less, 20 wt% or less, 15 wt% or less or 10 wt% or less. In other embodiments, the amount of ionic liquid is 90 wt% or less, 80 wt% or less, 75 wt% or less, or 60 wt% or less. In other embodiments, the amount of ionic liquid is 50 wt% or more, 75 wt% or more, 85 wt% or more or 90 wt% or more. It will be appreciated that is can be desirable, if possible, to employ lower levels of ionic liquids which presently are generally relatively more expensive than dipolar aprotic solvents other than ionic liquids.
  • an acid other than a phenylboronic acid is added to the reaction mixture to facilitate hydrolysis of polymeric carbohydrates (cellulose, xylose, etc.).
  • the amount of acid can range from dilute acid up to 5% by weight of solvent. Dilute acid is typically employed, where added acid is less than 1% by weight of solvent in the reaction mixture.
  • a Bronsted acid is employed.
  • the acid is an organic acid or a mineral acid, including, among others, acetic acid, phosphoric acid, HC1, sulfuric acid, and nitric acid.
  • the invention provides a low-temperature ( ⁇ 250 °C), nonenzymic route from lignocellulosic biomass to fuels. Most other chemical methods for the conversion of
  • lignocellulosic biomass to fuels use extreme temperatures to produce pyrolysis oil or synthesis gas, incurring substantial energy costs.
  • This low temperature chemical conversion also has inherent advantages over bioprocessing for cellulosic fuels and chemicals. Fermentation of lignocellulosic feedstocks requires saccharification through extensive pretreatment, fragile enzymes, and engineered organisms.
  • the processes of the invention process use simple, inexpensive catalysts to transform cellulose and biomass into a valuable product in an ample yield.
  • the present method can, for example, generate over 40% yield of HMF from cellulose and total yields of HMF and furfural of over 30% from corn stover in one step.
  • Biomass components that cannot be converted into HMF such as lignin, can be reformed to produce 3 ⁇ 4 for HMF hydrogenolysis or burned to provide process heat (Navarro et al, 2007).
  • Furan products can be readily isolated from the reaction mixtures herein by methods that are well-known in the art. Additionally, if desired, isolated furan products can be further purified by methods that are well-known in the art.
  • a catalyst for producing furans from a carbohydrate substrate comprises a 2-substituted phneylboronic acid, particularly a 2-carboxy or a 2-alkoxycarbonyl phenylboronic acid.
  • the phenylboronic acid can be in the form of a salt or a hydrate, particularly a monohydrate.
  • the catalyst comprises a 2-substituted phenylboronic acid (1) wherein the 2-substituted phenylboronic acid is immobilized on a surface; (2) wherein the catalyst further comprises magnesium[II] or calcium[II] or (3) wherein the 2-substituted phenylboronic acid is immobilized on a surface and the catalyst further comprises magnesium[II] or calcium[II].
  • magnesium[II] or calcium[II] can be in the form of a salt, particularly a halide salt.
  • the salt may be hydrated.
  • the catalyst may comprise water to enhance yield of furan.
  • the catalysts may contain water such that the molar ratio of H 2 0 to magnesium[II] or calcium[II] or a mixture thereof is 0.5 to 10.
  • the 2-substituted phenylboronic acid is covalently linked to a surface, such as a resin.
  • the catalyst is capable of transforming a carbohydrate substrate into a furan in a polar aprotic solvent other than an ionic liquid, an ionic liquid or a mixture thereof.
  • the catalyst comprises a 2- substituted phenylboronate pf formula I.
  • the catalyst comprises a phneylboronate of formula I wherein R is a hydrogen or an alkyl group having 1-3 carbon atoms.
  • R is a hydrogen or an alkyl group having 1-3 carbon atoms.
  • the molar ratio of 2-substituted phenylboronate to magnesium[II], calcium [II] or a mixture thereof is 0.5 to 5.
  • the molar ratio of 2-substituted phenylboronate to magnesium[II], calcium [II] or a mixture thereof is 1 to 5.
  • the catalyst consists essentially of a 2-substituted phenylboronic acid (1) wherein the 2-substituted phenylboronic acid is immobilized on a surface; (2) wherein the catalyst further comprises magnesium[II] or calcium[II] or both (1) and (2).
  • the 2-substituted phenylboronic acid can have formula I and more specifically can have formula I wherein R is a hydrogen or an alkyl group having 1-3 carbon atoms.
  • Catlaysts of this invention can be employed to produce furans, particularly HMF and furfural, from carbohydrates, particularly glucose and cellulose.
  • the invention provides carbohydrate dehydration medium which comprises a catalyst of the invention as described herein in combination with a polar aprotic solvent other than an ionic liquid, an ionic liquid or a mixture thereof as described herein.
  • Monosaccharides include hexoses (6-carbon
  • Exemplary hexoses include aldohexoses and ketohexoses, exemplified, among others, by glucose, mannose, galactose. fructose, sorbose and tagatose, particularly the naturally-occurring D-isomers thereof.
  • Exemplary pentoses include aldopentoses and ketopentoses, exemplified, among others, by arabinose, ribose, xylose, ribulose and xylulose, particualry the naturally-occurring D-isomers thereof.
  • Disaccharides include reducing and non-reducing saccharides, exemplary disaccharides, include among others, sucrose, lactose, cellobiose, maltose, and xylobiose.
  • Oligosaccharides are oligomers of monosaccharides.
  • oligosaccharide is used to refer to those species having 2-20 monomer repeating units and more specifically to those having 2-10 repeating units.
  • Oligosaccharides can be hexose oligosaccharides, particularly homo- oligosaccharides where the repeating units are the same hexose, e.g., glucose oligomers.
  • Oligosaccharides can be pentose oligosaccharides, particularly homo-oligosaccharides where the repeating units are the same pentose, e.g., xylose oligomers. Oligosaccharides may however contain mixtures of hexose and /or pentose monomers. Oligosaccharides can be derived from natural sources, for example, by application of various physical, chemical or enzymatic treatments or can be produced by fermentation or other microbial action.
  • cellulose is used broadly herein to include cellulose from any source and includes alpha-cellulose, beta-cellulose and gamma-cellulose and mixtures thereof.
  • Cellulose can be characterized by its degree of polymerization (DP, average number of anhydroglucose units) which can range from tens of thousands to hundreds, e.g., 10,000-12,000 to 300.
  • DP degree of polymerization
  • Cellulose as used herein also refers to underivatized cellulose or derivatives of cellulose, such as ethyl- or methylcellulose, hydroxyalkyl cellulose (e.g., hydroxypropyl cellulose), carboxymethylcellulose, or mixtures thereof.
  • the method of this invention is particularly useful for cellulose or cellulose derivatives which are water-insoluble.
  • the method of this invention is particularly useful for cellulose derived without chemical modification from natural sources.
  • Cellulose preferred for this invention contains less than 20% by weight of water and more preferably contains 15% by weight or less of water.
  • the water- content of cellulose can be determined and lowered by methods that are known in the art.
  • Lignocellulose or lignocellulosic material may be pre-treated by physical methods (grinding, chopping or mashing) or by chemical or biological (e.g., enzymatic) methods as are known in the art which may increase the accessibility of cellulose or other biomass
  • Lignocellulosic materials include, among others, wood residues, paper waste, agricultural residue and energy crops (e.g., woody grasses, such as switch grass or Miscanthus).
  • Lignocellulose and lignocellulosic material may contain water.
  • Preferred lignocellulose contains less than 20% by weight of water and more preferably contain 15% by weight or less of water.
  • the water-content of such materials can be determined and can be lowered by methods that are known in the art.
  • the methods of the present invention are useful for generation of HMF from high-cellulose lignocellulose materials, such as newspaper, paper towels and other paper products or waste products and cotton.
  • HMF prepared by methods herein can be employed as a source of various derivatives which are prepared by art-known methods. As shown in Scheme 3 (FIG. 3) HMF can be converted to other useful fuels or chemicals, particularly DMF.
  • the invention also provides a method of making useful fuels or chemicals in addition to HMF and furfural. Such methods comprise, as a first step, making HMF or furfural by a method of this invention from a carbohydrate or carbohydrate feedstock and thereafter converting HMF or furfural to other useful fuels or chemicals.
  • the invention provides a method for making DMF by conversion of HMF made by the methods of this invention.
  • HMF is converted to DMF via hydrogenolysis.
  • hydrogenolysis of HMF to DMF is conducted employing a copper catalyst and particularly using a copper-ruthenium catalyst or a copper chromite catalyst.
  • HMF can be converted to other useful species as is known in the art and as illustrated in FIGS 1- 3.
  • HMF can be reduced to levulinic acid or can be oxidized to 2,5- furandicarboxylic acid, by methods that are well-known in the art.
  • furfural made by the methods herein can be converted by art- recognized methods to useful chemical species.
  • furfural can be reduced to furfuryl alcohol which in turn is a precursor of various chemical products, including among others furan resins.
  • Furfural can be converted to tetrahydrofuran (THF), methyltetrahydrofuran (M-THF) and tetrahydrofurfuryl alcohol (THF A).
  • furfural can be converted to 1,5, pentane diol (Yu et al. 2011).
  • HMF and furfural prepared by the methods of this invention can be employed in condensation reaction (e.g., aldol condensation reactions) to generate more complex chemical species.
  • Molecules disclosed herein may contain one or more ionizable groups [groups from which a proton can be removed (e.g., -COOH) or added (e.g., amines) or which can be quaternized (e.g., amines)]. All possible ionic forms of such molecules and salts thereof are intended to be included individually in the disclosure herein. With regard to salts of the compounds herein, one of ordinary skill in the art can select from among a wide variety of available counterions those that are appropriate for preparation of salts of this invention for a given application. In specific applications, the selection of a given anion or cation for preparation of a salt may result in increased or decreased solubility of that salt.
  • any recitation herein of a phrase “comprising one or more claim element” e.g., “comprising A and B
  • the phrase is intended to encompass the narrower, for example, “consisting essentially of A and B” and “consisting of A and B.”
  • the broader word “comprising” is intended to provide specific support in each use herein for either “consisting essentially of or “consisting of.”
  • the invention illustratively described herein suitably may be practiced in the absence of any element or elements, limitation or limitations which is not specifically disclosed herein.
  • the estimated water-content of cellulose employed is 0-2% by weight as determined by measuring weight loss after heating to 140 °C. Milled and sieved corn stover and AFEX-treated corn stover were generously provided by B. E. Dale and co-workers (see U.S. patents 4,600,590 and 6,106,888 for a description of the AFEX process.) The estimated water-content of corn stover employed is 5—10% by weight of corn stove as
  • concentrated under reduced pressure refers to the removal of solvents and other volatile materials with a rotary evaporator under reduced pressure provided by a Welch 2025 self-cleaning dry vacuum system while maintaining the water-bath temperature below 50 °C except where noted.
  • high vacuum refers to a vacuum of ⁇ 0.1 torr achieved by a Welch mechanical belt-drive oil pump.
  • speed vacuum refers to spinning samples in a UVS400 Universal Vacuum System from Thermo Scientific (Waltham, MA) under reduced pressure provided by a Welch 2042 DryFast vacuum system.
  • NMR spectra were acquired with a Bruker DMX-400 Avance spectrometer ( 1 H, 400 MHz; 13 C, 100.6 MHz) at the National Magnetic Resonance Facility at Madison (NMRFAM). NMR spectra were obtained at ambient temperature unless indicated otherwise. Values of the coupling constant J are given in Hertz. Mass spectrometry was performed with a Micromass LCT (electrospray ionization, ESI) in the Mass Spectrometry Facility in the Department of Chemistry. Analytic Methods. Reaction products were analyzed by HPLC and quantitated using calibration curves generated from commercially available standards. Product concentrations were calculated from HPLC-peak integrations, which were then used to calculate molar yields.
  • ESI electrospray ionization
  • Table 1 A lists results using boron/magnesium systems to catalyze the conversion of glucose to HMF in N,N-dimethylacetamide (DMA) or the ionic liquid, lethyl-3-methylimidazolium chloride ([EMIMJCl).
  • DMA N,N-dimethylacetamide
  • [EMIMJCl] lethyl-3-methylimidazolium chloride
  • Phenylboronic acids having a 2-carboxylate in particular showed a significant increase in yield of HMF over that obtained with MgCl 2 6H 2 0 alone.
  • Table 1A also provides a comparison of the reaction in the presence of various salts other than MgCl 2 , including halide salts of lanthanide metals (La and Ce), transition metals (Cr, Cu, Fe, Mo, and Zn), alkali metals (Li, Na, K, Cs and Rb) as well as other magnesium halides and an exemplary calcium halide.
  • the counterion of the magnesium salt did not appear to play a major role, as hydrated MgBr 2 and Mgl 2 were also effective in mediating the conversion. Calcium chloride also exhibited a significant
  • Tables 1C and ID list results from Table 1A and additional experiments conducted as described in Table 1 A to provide a comparison of conversion of glucose to HMF in DMA employing MgCl 2 -6H 2 0 as a function of the phenylboronate employed.
  • 2- methoxycarbonylphenylboronic acid and 2-ethoxycarbonylphenylboronic acid both promote significant levels of HMF formation from glucose in the absence of added salt or water.
  • Other substituted phenylboronic acids 3-carboxyphenylboronic acid, and trifluormethyl-substituted phenylboronic acids are also observed to promote HMF formation from glucose in the absence of added salt or water.
  • 2-methoxyphenylboroic acid, 5-amino-2- hydroxymethylphenylboronic acid, 2,6-dimethylphenylboronic acid, 3-carboxy-5-nitrophenylboronic acid, 4-carboxyphenylboronic acid and 2-carboxyphenylboronic acid promote relatively low levels of HMF formation from glucose under the conditions tested.
  • Table IE lists results from Table 1A and additional experiments conducted as described in Table 1A to provide a comparison of conversion of glucose to HMF in DMA employing hydrated salts. These results can be compared with those from Table IB (see Table 1H for selected
  • Table 1G lists results from Table 1A and may include additional experiments conducted as described in Table 1A. Table 1G provides a comparison of the effect of catalyst and salt concentration on conversion of glucose to HMF.
  • Table 2A lists results for the conversion of certain mono- and disaccharides (other than glucose and cellobiose) to HMF and furfural.
  • phenylboroic acid in the presence of magnesium ion and water in both a polar aprotic solvent other than an ionic liquid (e.g., DMA) and ionic liquid (e.g., [EMIMJCl.)
  • a polar aprotic solvent other than an ionic liquid e.g., DMA
  • ionic liquid e.g., [EMIMJCl.
  • Pentose sugars xylose and arabinose
  • Table 2B lists results for the conversion of fructose to HMF. Yields presented in Tables 2A and B are for unoptimized reaction conditions.
  • Tables 2C and 2D list results for the conversion of certain ketohexoses (including fructose) and certain aldohexoses (including glucose). Yields of 50% or more of HMF are observed from conversion of psicose, fructose, sorbose, glucose, mannose, gulose, idose, and galatose.
  • the variance of the conditions required to achieve the best HMF yields suggests differing levels of dehydration activity for the three boronic acids.
  • the 2-ethoxycarbonylphenylboronic acid has the highest dehydration capacity of the three, followed by 2-methoxycarbonylphenylboronic acid and then 2-carboxyphenylboronic acid.
  • the yields varied for the different ketohexoses, with fructose typically giving the highest HMF yields, followed by sorbose, psicose, and tagatose. It is possible that these differences are a result of the differing isomeric equilibria of the sugars. According to previous studies, fructose predominately exists in a furanose form in an organic medium, as does psicose. (Binder, J. B.; Cefali, A. V.; Blank, J. J.;
  • the methods of the invention can be employed to dehydrate to HMF D-hexose sugars that exist predominantly in either a furanose or pyranose isomeric conformation.
  • Certain phenylboronic acids alone can readily promote dehydration of D-hexoses that exist predominantly in the furanose form.
  • the apparent need for the presence of magnesium catalyst for conversion of D- hexoses that exist predominantly in the pyranose form suggest that the added salt (magnesium or calcium salt) facilitates isomerization of the pyranose forms to their furanose forms before dehydration to HMF.
  • Tables 3 A and 3B list results for the production of HMF from cellobiose and other glucose oligomers. The results observed are somewhat different than those observed for production of HMF from glucose.
  • HMF was produced on reaction of cellobiose with 2-carboxy-substituted phenylboronic acids in the presence of magnesium halide and water in both polar aprotic solvent and ionic liquid. Surprisingly, cellobiose reacted with 2-carboxyester substituted phenylboronic acids in DMA to generate high yields of HMF (-40-50%) without addition of magnesium halide or water. HMF formation was observed with cellobiose, cellotriose, cellotetraose, maltose, sucrose and inulin.
  • Acid catalysis is often necessary to hydrolyze cellulosic materials to access the monomeric glucose before conversion to HMF can occur. It is thus surprising that higher yields of HMF were obtained using the 2-methoxycarbonyl- and 2-ethoxycarbonylphenylboronic acids alone than in tandem with MgCl 2 6H 2 0 (Tables 3A and 3B). While the phenylboronic acids were apparently able to bind the cellobiose and facilitate hydrolysis and conversion to HMF, it seemed that coordination of the phenylboronic acid makes the conversion facile for only one monomer per saccharide, as the yields were always below 50%.
  • Table 4 lists results for conversion of glucose and cellobiose with additional 2-substituted phenylboronic acids.
  • the structures of these additional phenylboronic acids are illustrated in Fig. 4.
  • Phenylboronates having 2-carboxy and 2-methoxycarbonyl groups provide good HMF yields.
  • Phenylboronates having 2-ethoxycarbonyl groups typically provide the highest activity in carbohydrate conversion reactions. The effect of additional or alternative substitution on activity is examined in Table 4.
  • Carboxyl phenylboronic acids with an additional substitution were examined to see the effect of modifying the electronics of the aryl ring and determine the influence on HMF yields. Additional substitutions such as a trifluoromethyl, methoxy, fluoro and chloro resulted in an increase in HMF yields (Table 4). The addition of a fluoro group at the 5-position, however, resulted in a drastic decrease in HMF yields. This may be due to high reactivity that caused degradation of the HMF product. In general, the addition of inductively electron-withdrawing substituents results in an enhancement in HMF yields. The increase in yields could, for example, result from an increased association of the phenylboronic acids with the sugar due to a decrease in the electron density at the boronic acid moiety.
  • Glucose (51.6 mg, 286 ⁇ ), 2-carboxyphenylboronic acid (47.3 mg, 285 ⁇ ) or other phenylboronic acids (as indicated) and MgCl 2 6H 2 0 (145.5 mg, 716 ⁇ ) were mixed in DMA (N,N-dimethylacetamide, 500 mg) or [EMIMJCl (1 ethyl-3-methylimidazolium chloride, 500 mg).
  • the reaction mixture was heated at a selected temperature, e.g., 120 °C for a selected time, e.g., 4 h. At 1-h intervals, aliquots of the reaction mixture were removed for HPLC analysis.
  • HMF yield dependence on the H 2 0 to Mg molar ration is shown.
  • HMF yield generally increases with increasing water, but levels off as the H 2 0 to Mg(II) molar ratio approaches 8-9.
  • Experiments (data not shown) were also conducted in the presence of diaza-18-crown-6 at 1 equiv relative to Mg(II). The presence of the complexing agent was found to prevents Mg(II) from facilitating the conversion of glucose to HMF. This indicates that Mg(II) facilitates the conversion of glucose to HMF.
  • Example 3 Synthesis of HMF from Cellulose and Lignocellulose.
  • Tables 5A-5D list results for the production of HMF from cellulose in ionic liquid.
  • HMF was formed in generally good yield by reaction of cellulose in ionic liquid in the presence of the 2- carboxy-substituted phenylboronic acid, magnesium salt, water and dilute mineral or organic acid (less than 1% by weight).
  • Highest yields of HMF (-40%) were observed in reactions in the presence of 2-carboxyesters of phenylboronic acid, magnesium halide (e.g., magnesium chloride), water (added as hydrated magnesium salt) and dilute mineral acid, e.g., H 2 S0 4 or HC1 (where "dilute" means less than 1% by weight of ionic liquid).
  • Table 6 lists the results for the production of furans (HMF or furfural) from lignocellulose in the presence of 2-carboxysubstituted ester phenylboronic acid, magnesium salt, water and dilute acid (less than 1% by weight) in ionic liquid.
  • Lignocellulose was in the form of untreated corn stover or corn stover that was pretreated by ammonia fiber expansion (AFEX).
  • An 18% yield of HMF and 15% yield of furfural were obtained from corn stover using 2-methoxycarbonyl- phenylboronic acid with MgCl 2 -6H 2 0 and sulfuric acid or HC1.
  • a 14%> yield of HMF and 21 > yield of furfural were obtained from AFEX-pretreated corn under analogous conditions. Yields in Table 5 are for unoptimized reaction conditions. Substrate loading in these experiments ranged from 4-5 wt%> with respect to ionic liquid.
  • Table 7 lists results for the conversion of glucose and cellobiose to fructose as mediated by MgO and 2-carboxyphenylboronic acid and corresponding esters.
  • DMA polar aprotic solvent
  • [EMIMJCl ionic liquid
  • 2-substituted carboxyesters of phenylboronic acid did not exhibit any significant enhancement of fructose generation compared to the 2- carboxyphenylboronic acid.
  • Mg metal powder and MgS0 4 were also used in attempted conversions, but yielded only an insignificant amount of fructose.
  • cellulose where dilute mineral acid was also added, no fructose was detected by HPLC. The cellulose was observed to react to some extent to form insoluble humins and other unidentified products.
  • Glucose (49.5 mg, 275 ⁇ 1), 2-carboxyphenylboronic acid (45.9 mg, 277 ⁇ ) or other phenylboronic acid (as indicated) and MgO (36.6 mg, 908 ⁇ ) were mixed in DMA or
  • FIG. 5 illustrates exemplary immobilization of dicarboxylphenylboronates on an amine resin (with -NH 2 functional group) such as a NovaPEG resin from EMD4Biosciences (EMD Chemicals) or a TentaGel® Resin from RAPP Polymere.
  • an amine resin such as a NovaPEG resin from EMD4Biosciences (EMD Chemicals) or a TentaGel® Resin from RAPP Polymere.
  • the boronic acid, HOBt, HBTU and DIEA are used in excess relative to the resin, more specifically, exemplary amounts employed are 4 equivalents relative to resin of the phenylboronic acid, HOBt, HBTU and 8 equivalents of DIEA.
  • the phenylboronic acid, HOBt, and HBTU are dissolved in N,N-dimethylformamide (DMF), and DIEA is then added. Argon gas is bubbled through the solution for 15 min, to form activated carbonyls on the boronic acid.
  • the resin is then added and reacted with bubbling argon at room temperature for 2 h. The solution is then removed via vacuum filtration, and the resin is washed with DMF.
  • This general strategy can be employed with various substituted phenylboronates and various resins which can couple with a carboxylic acid group.
  • the reactions of Scheme 5 can also be combined with initial protection of the phenylboronic acid (as exemplified in Scheme 6 or employing boronic acid protecting groups (pinacol, pinanediol or more generally an alkyl diol) that are known in the art) prior to immobilization.
  • the protecting group(s) can be removed or retained until desired to employ the immobilized phenylboronic acid. Retention of protecting groups on the immobilized
  • phenylboronic acid can enhance shelf-life of the immobilized catalyst.
  • Scheme 6 illustrates an exemplary method for immobilization of 2- carboxyphenylboronic acid.
  • 2,4-dimethoxycarbonyl phenylboronic acid is treated with base to form the corresponding oxaborole, which can be isolated as a salt.
  • the oxaborole is then protected with an appropriate protecting group, e.g., pinacol, pinanediol or a diol, such a propylene glycol, and the 4-carboxylic acid group is activated by reaction with N- hydroxysuccinimide to form an N-hydroxysuccinimide ester.
  • an appropriate protecting group e.g., pinacol, pinanediol or a diol, such a propylene glycol
  • the activated ester is then be reacted with an amino functionalized resin, e.g., 0-(2-aminoethyl)polyethylene glycol resin to immobilize the protected oxaborole on the resin.
  • the oxaborole is then deprotected , e.g., with trifluoroacetic acid (TFA/H 2 0) to provide the immobilized 2-carboxyphenylboronic acid.
  • TFA/H 2 0 trifluoroacetic acid
  • the immobilized 2-carboxyphenylboronic acid can be converted if desired to 2-methoxycarbonyl or the 2-ethoxycarbonyl derivative by methods that are well known in the art.
  • glucose-2-d was converted into HMF by 2-ethoxycarbonylphenylboronic acid and
  • the reaction mixture was heated at 105 °C for 4 h, placed under high vacuum overnight to remove DMA, extracted with ethyl acetate, concentrated under reduced pressure, and analyzed by 1H NMR spectroscopy.
  • the aldehyde peak of HMF (9.56 ppm) showed ⁇ 5% deuterium retention, indicating that the isomerization mechanism from glucose to fructose is not a 1 ,2- hydride shift.
  • Glucose (100.5 mg, 558 ⁇ ) and 2-ethoxycarbonylphenylboronic acid (120.0 mg, 619 ⁇ ) were dissolved in DMA (1064 ⁇ ,), and D 2 0 (500 ⁇ ) was added to exchange any labile protons with deuterons. This mixture was then concentrated under reduced pressure to remove D 2 0 and H 2 0. The D 2 0 exchange was repeated.
  • Phenylboronic acids such as 2-hydroxymethylphenylboronic acid, known to have high affinity for sugar binding were not found to significantly enhance sugar conversion to HMF in the methods of this invention.
  • carboxyl phenyboronic acids which have been reported (Berube, M; Dowlut, M.; Hall, D. G. J. Org. Chem. 2008, 73, 6471; Dowlut, M.; Hall, D. G. J. Am. Chem. Soc. 2006, 128, 4226) to have weak affinity for binding to fructose and glucose significantly enhance sugar conversion to HMF by the methods herein.
  • the binding affinity of various phenylboronic acids has been determined previously under aqueous conditions (Berube et al. 2008 and Dowlut et al. 2006). Reactions of the present invention employ organic solvents and ionic liquids and the binding affinities may be significantly different in such solvents.
  • phenylboronic acids and sugars were dissolved in DMSO-d 6 , which served as a deuterated organic solvent substitute for DMA. Both 2-carboxyphenylboronic acid and the unsubstituted phenylboronic acid were observed to form anhydride structures which can be broken up with the addition of water. When fructose and glucose were added, complex formation between 2- carboxyphenylboronic acid with both fructose and glucose was observed. Typically, the aryl hydrogens of the boronic acid demonstrate a distinct shift in their chemical shifts upon complexation to a sugar. [Berube et al. 2008; Dowlut et al. 2006.]
  • MgCl 2 *6H 2 0 was added and the spectra of the phenylboronic acids were reexamined in the presence of fructose and glucose to mimic reaction conditions where HMF formation was enhanced. While some peak broadening was observed, no significant changes to the overall spectra were observed. The addition of MgCl 2 , 6H 2 0 does not appear to affect the boronic acid-sugar binding.
  • the anionic boronate was retained on the resin and eluted with aqueous base (e.g., aqueous NH 4 HCO 3 (1 M)) to yield purified boronate. Recovered catalyst was found to retained catalytic activity. This strategy is inapplicable to the substituted phenylboronic acid catalysts that have low water solubility and high solubility in ethyl acetate such as 2- alkoxycarbonyl phenylboronic acids.
  • aqueous base e.g., aqueous NH 4 HCO 3 (1 M)
  • sucrose Antal, M. J., Jr.; Mok, W. S. L.; Richards, G. N. Carbohydr. Res. 1990, 199, 91- 109.
  • Phase modifiers promote efficient production of hydroxymethylfurfural from fructose.
  • Furfural Hemicellulose/xylose-derived biochemical. Mamman, A. S.; Lee, J. -M.; Kim, Y. -C; Hwang, I. T.; Park, N. -J.; Hwang, Y. K.; Chang, J. -S. (2008) Biofuels, Bioprod. Biorefm., 2, 438-454.
  • Boronic acid-functionalized nanoparticles Synthesis by microemulsion polymerization and application as a re-usable optical nanosensor for carbohydrates, Cannizzoa, C,
  • Mol% and molar yield are relative to the glucose in the reaction mixture.
  • Mol% and molar yield are relative to the glucose in the reaction.
  • Glucose was at 10wt% relative to DMA. Mol% and HMF yield are relative to glucose.
  • ND not determined, because HM F and the boronic acid have the same HPLC retention time.
  • Table IE HM F from glucose in DMA using hydrated metal chlorides and boronic acids
  • Mol% and molar yield are relative to the glucose in the reaction.
  • Mol%, molar yield, and water molar equivalents are relative to the glucose in the reaction.
  • 2-Carboxyphenylboronic acid was used at 100 mol% and MgCI 2 at 200 mol% relative to glucose.
  • Glucose and boronic acid were 10 wt% relative to solvent. Mol% and HMF yield
  • Reaction mixture contained 2-carboxyphenylboronic acid (100 mol%) and MgCI 2 -6H 2 0 (200 mol%). Mol% and molar yields are relative to the sugar. Table 2B. Fructose to HMF conversion with boronic acids
  • Mol% and molar yield are relative to the fructose in the reaction.
  • Table 2D Aldohexose conversion using 2-carboxyl phenylboronic acids.
  • Wt% is relative to the [EMIM]CI. Mol% is relative to glucose in the cellulose in the reaction mixture; AcOH is acetic acid. Table 5B. Catalyst concentration determination for cellulose to HMF co ⁇ in [EMIMJCI
  • Wt% is relative to the [EMIMJCI. Mol% is relative to the cellulose in the reaction.
  • Wt% is relative to the [EMIMJCI. Mol% is relative to the cellulose in the reaction.
  • Table 5D Selected Data for Conversion of Cellulosic Substrates to HMF in Ionic Liquid
  • Substrates were at 5wt% relative to the ionic liquid. Wt% is relative to the ionic liquid. Mol% and HMF yield (HPLC)
  • Mol% is relative to the cellulose content in the corn stover.
  • H 2 S0 4 was added at less than 1 % by weight of solvent.
  • Mol% is relative to glucose, glucose in cellobiose or estimated glucose in cellulose in the reaction mixture.

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Abstract

Cette invention concerne des procédés et des compositions catalytiques de formation de furanes à partir d'hydrates de carbone. Un substrat d'hydrate de carbone chauffe en présence d'un acide phénylboronique 2‑substitué (son sel ou son hydrate) et éventuellement d'un sel d'halogénure de magnésium ou de calcium. La réaction est effectuée dans un solvant aprotique polaire autre qu'un liquide ionique, un liquide ionique ou un mélange. Une certaine quantité d'eau ajoutée à la réaction peut augmenter le rendement des furanes.
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WO2017170976A1 (fr) * 2016-04-01 2017-10-05 和光純薬工業株式会社 Solution électrolytique contenant des ions magnésium
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WO2016022201A1 (fr) * 2014-08-07 2016-02-11 Thomas Tao Procédés de conversion de glucides en oxo-hydrocarbures et furanes
CN105688988B (zh) 2014-12-16 2018-11-27 财团法人工业技术研究院 糠醛化合物的氧化反应催化剂及糠醛化合物的氧化方法
FR3043081B1 (fr) 2015-11-02 2017-12-08 Ifp Energies Now Procede de production de 5-hydroxymethylfurfural en presence d'un catalyseur acide de lewis et/ou d'un catalyseur base heterogene et d'un catalyseur organique homogene acide de brønsted en presence d'au moins un solvant polaire aprotique

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